Abstract

Gas separations with faujasite zeolite membranes have been examined using the method of molecular dynamics. Two binary mixtures are investigated, oxygen/nitrogen and nitrogen/carbon dioxide. These mixtures have been found experimentally to exhibit contrasting behavior. In mixtures the ideal selectivity (pure systems) is higher than the mixture selectivity, while in the mixture selectivity is higher than the ideal selectivity. One of the key goals of this work was to seek a fundamental molecular level understanding of such divergent behavior. Our simulation results (using previously developed intermolecular models for both the gases and zeolites investigated) were found to replicate this experimental behavior. By examining the loading of the membranes and the diffusion rates inside the zeolites, we have been able to explain such contrasting behavior of and mixtures. In the case of mixtures, the adsorption and loading of both and in the membrane are quite competitive, and thus the drop in the selectivity in the mixture is primarily the result of oxygen slowing the diffusion of nitrogen and nitrogen somewhat increasing the diffusion of oxygen when they pass through the zeolite pores. In systems, is rather selectively adsorbed and loaded in the zeolite, leaving very little room for adsorption. Thus although continues to have a higher diffusion rate than even in the mixture, there are so few molecules in the zeolite in mixtures that the selectivity of the mixture increases significantly compared to the ideal (pure system) values. We have also compared simulation results with hydrodynamic theories that classify the permeance of membranes to be either due to surface diffusion,viscous flow, or Knudsen diffusion. Our results show surface diffusion to be the dominant mode, except in the case of binary mixtures where Knudsen diffusion also makes a contribution to transport.